Process of manufacturing producer-gas.



No. 840,461 PATENTED JAN. 8, 1907. w. 11.. ADAMS & F.'-'POWELL. PROCESS OF MANUFACTURING PRODUCER GAs.

APPLIOATION FILED JUNE 20,1904.

UNITED s'm'rns, PATENT OFFICE,-

WlLLlAM H. ADAMS AND FREDERICK POWELLl OF PORTLAND, OREGON,

AESSlGNORS OF TWENTY-FlVE PER CENT. TO SAID ADAMS,'F1FTEEN PER GENT. TO SAID POWELL, AND SIXTY PER CENT. TO THE LADD ltlETALS (L'OMPANY, A CORPORATION OF OREGON.

PFRUOE$$ or MANUFACTURING PaoDuoan-hna.

Specification of Letters rams.

Application filed June 20,1904. Serial For 218,242-

I'Mentcd (Fan. 8, 1907.

or coke or from any ,of these substances mixed with petroleum, tars, asphaltu'm, as, in proper proportionsd what is generully'irnown as producer gas.

Producer-gas is now manufactured as follows: In one method the generator is supplied with fuel from the top, has a grate near the bottom to sustain the bodyof fuel, means for adinittins air under the ate, and an cxit pipc. at tile top for the delivery of gas'to the iurnaces,'wherein it iii burned by the addition of heated'air, or to the scrubbers and thence to gas-holders to -be used for other purposes. In this class of enerators the air passes upward through the ody of fuel, and

during the operation the contained. heat,

water-vapors, tars, &c., pass through the posit a considerab e amount of tar and free carbon or lampblack in their passe e to the point of consumption or to the scrub er. In this generator also the combustion in, the lower strata of the fuel reaches high heats, and in this zone many reactions take place by which the oxygen of the air, the carbon of the fuel, and the hydrogen of the water are brought into contact to produce gas. The fuel in the upper part of the generator is subjected to a gradu ally-increasing temperature, due to the combustion of the lower strata, so that distillation takes placein the upper part of the producer and continues atftem eralures increasing as the fuel. descends, w ere by all the water, whether free or hygroscopic, nearly all the volatile hydrocarbons, the tars,

and considerable unburned carbon in the form of lampblaclr. pass-outwiththe gas, When the gas", is not to "bajiinunediately' Our invention relates to the new process exit-pipe at the to of the generator and de-* tillation products, through scrubbers and other objectionable constituents are removed and also a considerable part of the volatile hydrocarbons. In this method of manufacture the gas produced varies matestituents and also in the quantity and has has been immediately burned, the loss taking place iii-scrubbers and washers being as power. In another form of generator the air-inlet is at the to gas at the bottom; the this form is likewise objectionable. The volatile hydrocarbons and moisture of the fuel in this construction are drawn down through the zone of combustiorrjust above the rate, and it is manidescent fuel at this place no possible dissociation of theseconstituente can take place; but such body of incandescent fuel cannot be maintained, because the downward draft bons reduces the temperature of the fire to'a point too low to accomplish-the reactions necessary for maki fixed gas. The air drawn into the fuel is diluted with elements which do not support combustion, but which greedily absorb the oxygen from the air at the temperature of dissociation, Consequently combustion rapidly diminishes in producers of this type with a constant feed anddownward draft. To carry on practicable and economical operations with this type of'producers, a series of two or more-of t cm are needed, so that the fires can be blown up during one interval and the gas made by reversingthe draft duringanothcr great care and watchfulness. Failure to reverse the draft at' the )ropcr instant results in the production of a large voluiue'of undccom osed water-Va of, tar, 'and. products of com stion diluted to the point "of being valueless.

Our invention is intended to supply a less expensive self-co1itained and general use Hui method of gas-production -which will perburned, it isnecessarytopass it, with the dis- I purifiers, whereby the tar, lampblack, and

rially in the percentage of its several con- 6o, only been successfully worked where the gas inuch'ns thirty-five per cent. of the calorific andthe outlet for the fest that without a suihcient body of incan-v carryin the water and volatile hydrocarinterval, an intermittent operation requiring ZOO mit the working of any class of-fuel containing sntlieient carbon to make a-hot tire, preferably the culrn coals, peat, sawdust, and all classes of waste wood that are easy to burn, and which will'be continuous and posi-- tive in its operations and capable of making gas of uniform composition.

We make use of a new form of generator in the practice of our process, the construction of which will be understood from the ac eoinpanying drawings, in which 4 Figure l is a VOILiCillSOC'tlOIl 0n the line A B of Fig. 2, and Fig. 2 is a horizontal section on the line D of Fig. 1.

The chamber P of the generator is prefer ablyelliptical in form and is elongated at the base just above the grate T, so .as to form an Increased area at thezone ol' incandescence.

' in this mannerwe insure an additional mass of fuel in. this zone whichwe find desirable to 1 thorou hly decompose and ii); the products of com ustion and thevolatile constituents of the fuel; The fuel isadnutted to the chamber of the generator by the feed device S, the operation of which will be. understood. S represents a valved feeden through which liquid hydrocarbons may be admitted tothe generator for enriching the gas.

A water-seal ash-pan is shown at and W is an air-inlet pipe having ports '10, through which the air passes to the fuel.

X is the outlet for the gas, and, as-will be seen. it is in the same horizontal plane practieally as the. air-inlet.

' generator, anr

W is an additional ai rinlct for supplying air through that portion of thegratcjnnnediately below the p orts W.

"N is a vertical diaphragm placed -transversely, across the bottom of the generator below the grate and extending downward into the water in the ash-pan 'lhis diaphra m limits the area of the grate through which air and steal'n are applied to the inlet,

W and forms a close junction at itsends with the depending skirt \-",.which surrounds the grate-space and extends down into the water of the aslupan. This shirt attends the water seal with the ash-pan and prevents the entrance. of the airto the bot-toinol the grate, except such as is admitted by the air-inlet' iicient'ln-ight abovpdhe grate with wood to act as lillltlllligfi On top of this is added suf ficient fuel of any desired character tobring the level somewhat .above' the gas-outlet.

of the generator.

and the amount of ments always found in The fireis then lighted through the pokeholes and increased by natural draft or the application of a gentle blast through the pipe W. All openings in the top of the generator are then closed substantially air-tight. The-fire quickly spreads across the bottom of the generator, igniting the fuel u) to the level of the top of the gas-outlet, as s own by the lines radiating from W. As soon as this is accomplished (ten or fifteen minutes being usually sull'icient) the blast is increased and a regular feed of fuel is begun, carebeing. taken to prevent the escape of gas at the top 1 i -The entire body of thefnel bet-ween the top of the gas-ont etis broughtgto a state of incandescence and afterward maintained. in

i that state, so that a steady output of the gas can be obtained, through the same and the quality of the gas be always within control of the operator by'choice in the kind and in' the quantity of fuel', t.he volume of air applied, ,nioisti1re i.n-tlie fuel or applied in the form of steam at Z.

grate and the. plane of the nthis process the reactions take place as 9:

in other producers-mamely, the union of the oxygen of the'air with the carbon or hydrogen of the fuel reducing carbonic acid and water-vapor, t \ese being decomposed in their passage horizontallvacross the bottom 5 of the generator through the bed of incandescent fuel and QSCftPlllg through the gasoutlet X in the form of carbonic 'oxidand hydrogen with the usual percentage of nitrogen and a small-amount olthe other elereducer-gas: In addition. to this-the volatile constituents of the fuel set free in the zone immediately above the zone of incandescence pass at once down ward into the latter in their pure statkaim- 'diluted with air, as in the caseoi the downdraft-producers referred to, and. not driven forward in a crude state with the other gases, as in the u'idraft-producers, but, on the centrary,;by tlieir iInI-nediate entrance into. the bed of incandescent fuel are at once converted into fixed. gases; the moisture being converted into, water-gais and the tars split up into permanent gaseous hydrocarbons and carbonic oxi'd.. I i

The bed of fresh fuel above the zone ofi candcsecnee, which is a very important t'cati'ireol' our process, is renewed, of course, as last as it set-t les into the zone of incandeseenec, and the form of the apparatus is such ,as to make it easy to maintain aconstant renewal of the fuel and the withdrawal of the. ash as last its-required, so as to maintain a unitorni continuation of the process. 5 It also enables us to maintain a zone of incandeseeirce ot'nnifo'rni depth and extent, and by the exact regulation of the volume-of air and the amount of fuel we are-enabledto in,-

sure a constanthigh temperature, and therefore a constant percentage of gas from a 1'30 known quantityof fuel. It is also practicable in our fresh fuel ad ftional 'fuelrich .in volatile These may be a (led with the solid fuelor separately, as desired, through the feeder S under proper control, or they ma us be sup- -:plied with an absorbent fuel, sue as sawdust, and

fed therewith. These volatile gases in their h the zone of 'mcandescence.

ere the gas is lean in combustibles, we b d may in this manner enrich it to any desired extent during its manufacture, and this pro- Icedure is not feasible or practicable in'other processes of manufacturing producer-gas.

The process can be carried on continuously or intermittently at will and can be practiced g o, in a single producer, and we obtain with one generator all that is accomplished by the more ex ensive used wit then .25

t and water-vaporsan 3O roducer-plants heretofore gas produced, whic of course, may vary somewhat in its constituents, is, however, substantially. free from objectionable constituents-such as tars volatile substances,

can be at once utilized for heating) boilers or'for. metallurgical fWOIk, or it can e cleansed in the usual manner at less expense and with no appreciable end, the a A bustion from the front portion.

2. The process of manufacture of gas conloss of valuable constltuents.

We claim 1. The improvement in the manufacture of producer-gas consisting in establishing a horizontal zone of incandescence in the lower portion of a long horizontal body of fuel, admitting air to one end only of the body and iving exit to the gas at the other mission of the air and the exit of the gas takin place at the same level and in the plane of t e zone and suchexit being the only exit provided for the gas, whereby the rear portion of the incandescent fuel is caused to decompose the products of com- .sisting in forming along horizontal bodyof fuel, maintaimng the lower portion of said ody in an incandescent condition by the combustion of a'portion of its constituents by means of air admitted at one.end of the rocess to add to the bed of 1 u lication of parts. The- .fuel and at the same maker body and escaping at the opposite end, both inlet andoutlet being= -below the top :of the fuel-andfat'the same level and such exit bein the only exit provided for the as, and the girther decom osition ofthe'pro nets of combustion in t eir passage horizontally through the bed ofincandescent fuel and the addition of steam, thereby producin so-' called producer-gas with an additiona percentage of hydrogen.

he processof manufacture of as"consisting. in forming a long horizontal ody of fuel, maintaining the zlo veripbrtion' of said 0 y in an incandescent condition by the combustion of a portion of its constituents by means of air admitted at one end of the body and escaping at the opposite end, both inlet andoutlet-being below the top of the fuel and at the same level and such exit bein the only exit provided for, the as, and' v combustion in t w the urther decomposition-of the pro nets of eir passage horizontalliy throughithe bed of incandescent fuel, the a so-called producer and water gas and the addition to the said producer and .water as of thelvolatile constituents contained in iquid ue r 4. The process of manufacture of as consisting in forming a long horizontal ody of fuel, maintaining the lower portion of said ody in an incandescent condition by the combustion of a portion of its constituents by means of air admitted at one end of the body and escaping at the opposite end, both inlet and outlet. bein below the top of the level and such exit being the only exit rovided for the as, the addition to said bed of fuel of liquid fuels rich dition of steam, the generation thereby of v in volatile hydrocarbons, the further decomposition of the products of combustion in' 4 their passage horizontally through the bed of incandescent fuel, the addition of steam,

, the generation thereby of socalled producer and Water gas and the addition to the said producer and water gas of thevolatile constituentscontained in liquid fuel. 

